2018
DOI: 10.1016/j.renene.2018.01.057
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Numerical analysis of wood biomass packing factor in a fixed-bed gasification process

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Cited by 38 publications
(18 citation statements)
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“…The reactor mainly had an internal diameter of 102 mm, an external diameter of 185 mm, and a bed length of 400 mm. A description of the experimental setup is presented in detail in previous works . The behavior of this reactor is similar to that of TLUD cookstoves operating only with primary air.…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…The reactor mainly had an internal diameter of 102 mm, an external diameter of 185 mm, and a bed length of 400 mm. A description of the experimental setup is presented in detail in previous works . The behavior of this reactor is similar to that of TLUD cookstoves operating only with primary air.…”
Section: Methodsmentioning
confidence: 99%
“…The two main changes on the chemical surface structure of biochars identified by Fang et al [39] are the dehydration and aromaticity. Thereby, in this work, the aromatic index was estimated as proposed by Brewer et al [40] according to Equation 4:…”
Section: Physicochemical and Thermal Characterizationmentioning
confidence: 99%
“…When the agreement between both experimental and simulated results is not sufficient, the model is usually later improved or even reformulated, aiming at obtaining results closer to the empirical ones . For example, Gonzalez et al found certain discrepancies among the predicted and experimental data for H 2 , CH 4 , and CO 2 during gasification in a fixed‐bed reactor, subsequently affecting the estimation of other dependent parameters, such as the heating value. In most of the cases, a review is assumed to be required in the model, regardless of the possible (and more probable) inaccuracy of the experimental reference data.…”
Section: Introductionmentioning
confidence: 99%
“…Non-experimental sensitivity analysis under various operating conditions is quite commonly applied, providing a deep insight into the process at minimum cost, while also facilitating design optimization. Detailed Computational Fluid Dynamics (CFD) calculations have been thoroughly used for the modeling of biomass gasification reactors [15,16]. Given that the goal of the model is to predict the overall process efficiency and the general behavior of the gasifier operation, simple 0-D global models are preferred.…”
Section: Introductionmentioning
confidence: 99%